US2504434A - Forming oxide coatings on aluminum - Google Patents

Forming oxide coatings on aluminum Download PDF

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US2504434A
US2504434A US724923A US72492347A US2504434A US 2504434 A US2504434 A US 2504434A US 724923 A US724923 A US 724923A US 72492347 A US72492347 A US 72492347A US 2504434 A US2504434 A US 2504434A
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aluminum
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Ralph B Mason
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Howmet Aerospace Inc
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Aluminum Company of America
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/60Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using alkaline aqueous solutions with pH greater than 8
    • C23C22/66Treatment of aluminium or alloys based thereon
    • C23C22/67Treatment of aluminium or alloys based thereon with solutions containing hexavalent chromium

Definitions

  • the invention is particularly applicable to processes embonate. In the use of such solutions, it is usually preferred, depending upon the ultimate properties desired in the coating and sometimes upon the presence or absence of other constituploying aqueous solutions of the carbonate type, 5 ents in the solution, to provide in the solution especially carbonate-chromate solutions, with a small quantity of an alkali metal chromate, or without, additions of polyvinyl alcohol or i. e. about 0.05 to 2.0 percent by weight. A various proteins.
  • chromate such as sodium or potassium chromate
  • the invention is concerned with artificial y is usually present in a ratio between about one produced oxide coatings on aluminum, and cerll) part chromate to two parts carbonate and about tain chemical treatments for producing them; one part chromate to thirty parts carbonate. and it is not concerned with electrolytic treat- Appropriate smaller amounts of sodium or potasments for producing oxide coatings.
  • slum dichromate have been employed to provide herein, the term aluminum includes pure aluthe desired chromate content in the solution. minum, commercial aluminum containing the In recent years, two improved carbonate type usual impurities, and aluminum base alloys.
  • a soluble salt of aluminum can be-dissolved in a coating solution of the carbonate type and the solution treated, either before or after or simultaneously with such addition, so as to produce therewith the desired aluminum complex in the solution, and also at least some precipitate of the desired hydrated alumina.
  • This improvement in the coating process can be achieved, in general, by preliminarily providing in the solution (1) a soluble salt of aluminum in an amount sufiicient to increase the aluminum content thereof by at least about 0.05 per cent by weight, or more if desired, and (2) a neutralizing compound (such as an alkali metal bicarbonate or hydroxide) selected to react with the aluminum salt in solution to produce a condition of alkalinity in the solution in which there is an appreciable amount of aluminum complex of low solubility in the solution adapted to be precipitated as hydrated alumina.
  • the neutralizingcompound is selected alumina, usually at a value near that which would be exhibited by the solution were the additions not made. They result in the formation of an appreciable amount of aluminum complex in the solution; and, especially in the case of the larger additions and when cooling is employed, they usually also result in the precipitation of an appreciable amount of hydrated alumina.
  • One class of soluble salts of aluminum which i can be employed in the practice of the invention is the class of soluble alkali metal aluminates.
  • the preferred member of this class is sodium aluminate, which may be added effectively in an amount by weight of about 0.15 to 0.5 per cent,
  • This addition increases the aluminum content of the solution by an amount on the order of that previously indicated as desirable.
  • the neutralizing compounds best employed with the aluminates are the soluble alkali metal bicarbonates, which may be added in an amount suflicient to increase the carbonate content of the solution by about 0.1 to 0.3 per cent by weight, or more if desired.
  • the preferred member of this class of compounds is sodium bicarbonate, which may be added effectively in an amount by weight of about 0.15 to 0.5 per cent, or more, depending on the amount of aluminate added.
  • the aluminate is alkaline in solution (tending to raise the pH of the solution), and that the bicarbonate has an acid reaction (tending to lower the pH of the solution). They react with each other insolution, producing some added alkalimetal carbonate, as well as the aluminum complex. The added carbonate does not interfere with the coating characteristics of the solution and, in fact, it merely raises the alkali metal carbonate content of the solution. If desired, the solution may be originally made up with an initial alkalimetal carbonate content less than that ultimately desired, according to the amount that will be formed in the preliminary treatment here described.
  • Neutralizing compounds other than the bicar bonates may also be employed with the aluminates.
  • carbon dioxide may be substituted for the bicarbonates.
  • alkali metal dihydrogen phosphates, bisulphates, bisulfites, and sulfur dioxide (or sulfurous acid) may be employed. In any case these neutralizing compounds should be employed in approximately the stoichiometric amounts for the neutralizing reaction with the aluminate.
  • Another class of soluble salts of aluminum which can be employed in the practice of the invention is the class of soluble normalaluminum salts.
  • the preferred member of this class is aluminum sulfate, but other similar aluminum salts such as the chloride or the. nitrate, or the like, may be found suitable.
  • Aluminum sulfate for example, may be added efiectively in an amount by weight of about 0.3to l per, cent, or more if desired, the weight being referred to the anhydrous salt. Hydrated aluminum sulfate will usually be employed and the corresponding larger weight of that form of aluminum sulfate would, of course, be added, the appropriate .actual weight of either form being contemplated herein.
  • the neutralizing compounds best employed with the normal aluminum salts are the soluble alkali metal hydroxides, which may be added in an amount sufiicient to increase the hydroxyl content of the solution by about 0.1 to 0.3 per cent by weight, or more if desired.
  • the preferred member of this class of compounds is sodium hydroxide which may be added efiectively in an amount by weight of about 0.2 to 0.7 per cent by weight, or more, depending on the amount of normal aluminum salt added.
  • the aluminum salt in this last class is acid in solution (tending to lower the pH of the solution), and that the hydroxide is alkaline (tending to raise the pH of the solution to a point favorable to formation of the aluminum complex). They react with each other in solution, producing an alkali metal salt, as well as the aluminum complex.
  • the alkali metal salt does not interfere with the coating characteristics of the solution, but it does not raise the alkali metal carbonate content of the solution.
  • Soluble aluminum salts other than the normal salts may also be added to the solution.
  • additional hydroxide is needed in the solution to neutralize the aluminum salt.
  • the provision of an acid salt and the necessary additional hydroxide in the solution is equivalent to the provision of a normal salt in the solution.
  • a basic aluminum salt is employed, part of the hydroxide required in the solution is supplied by the hydroxide content thereof.
  • the provision of part of the hydroxide by way of a basic salt and a smaller amount of alkali metal hydroxide is equivalent to the provision of a normal salt and a corresponding total amount of alkali metal hydroxide in the solution.
  • a typical coating solution including the firstmentioned class of soluble salts of aluminum might contain the following percentages by weight of coating and stabilizing constituents:
  • the adjustment and readjustment of the pH of the solution may take place as follows. If a solution of carbonate and chro mate only is first made up, it will exhibit a pH of about 11. If sodium aluminate is then added, the pH will rise above approximately 11.2. Then, if sodium bicarbonate is added, the pH will fall below about 10.5, slightly below the original value of 11. Likewise, if sodium hydroxide is first added, the pH will rise above approximately 11.6. Then, if the aluminum sulfate is added, the pH Will fall below about 10.5, slightly below the orig-- inal value of 11. Similar changes take place if? the order of adding the salt of aluminum and the: alkali, is reversed, in either case.
  • the two constituents listed last may well be added last;v the chromate addition, however, may be con veniently deferred to a point after the addition of aluminate or hydroxide.
  • the order between:
  • the stabilizing constituents are best added in the preferred amounts to a hot solution. held at temperatures above about F., prefer-- ably a solution held at about to F. Thereafter, the solution is best cooled, preferably to room temperature, to precipitate appreciable quantities of hydrated alumina. Then the solution may be reheated to temperatures suitable for coating, preferably temperature between about 175 and 195 F.
  • the improvement-comprising preliminarily providing in the solution a soluble salt of aluminum in an amount suiiicientto' increase the aluminum content of the solution byat least about 0.05 per cent by weight and a neutralizingcompound reactive with the aluminum salt whereb to produce a condition of alkalinity in the solution in.
  • the improvement comprising preliminarily providing in the solution a; soluble salt of aluminum in an amount sufiicient'to increasethe aluminum con tentof thesolution by at least about 0.12 per cent b weight and a; neutralizing compound reactive with the aluminum salt whereby to produce a condition of alkalinity in the solution in which there is an appreciable amount of aluminum complex of low solubility in the solution adapted to be precipitated as'hydrated alumina; the neutralizing compound'being provided in an amount approximating the stoichiometric amount for the reaction with the amount of thesalt of aluminum provided.
  • alkali metalbicarbonate being provided in an amount approximating the stoichiometric amount for reaction with the amount of alkali metal aluminate provided so that an appreciable amount of "aluminum complex of low solubility'is formed 'in the solution adapted to be precipitated as hydrated alumina.
  • a process for forming an oxide coating on aluminum by treating in an aqueous solution containing about 0.5 to 6 per cent by weight of alkali metal carbonate comprising preliminarily providing in the solution a soluble normal aluminum salt in an amount sufficient to increase the aluminum content of the solution by at least about/0.05 per cent'by Weight and a soluble alkali metal hydroxide in an amount suflicient to increase thehydroxyl content of the solution by.
  • a process for forming an oxide coating on aluminum by treating in a hot aqueous solution containing about 1.5 to 2 per cent by weight of sodium carbonate and up to about 0.75 to 1 per cent by weight of an alkali metal chromate.
  • the improvement comprising preliminarily providing in the hot solution about 0.8 per cent by weight of aluminum sulfate and about 0.5 per cent by weight of sodium hydroxide, so that an appreciable amount of aluminum complex of low solubility is formed in the solution adapted to be precipitated as hydrated alimiina, then cooling the solution to about room temperature so as to facilitate precipitation of an appreciable amount of hydrated alumina, and then reheating the solution for coating.

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

Patented Apr. 18, 195i} UNITED STATES FORMING OXIDE COATINGS N ALUMINUM Ralph B. Mason, New Kensington, Pa., assignor to Aluminum Company of America, Pittsburgh,
TENT OFFICE Pa., a corporation of Pennsylvania No Drawing. Application January 28, 1947, Serial No. 724,923
metal in chemical coating solutions. The invention is particularly applicable to processes embonate. In the use of such solutions, it is usually preferred, depending upon the ultimate properties desired in the coating and sometimes upon the presence or absence of other constituploying aqueous solutions of the carbonate type, 5 ents in the solution, to provide in the solution especially carbonate-chromate solutions, with a small quantity of an alkali metal chromate, or without, additions of polyvinyl alcohol or i. e. about 0.05 to 2.0 percent by weight. A various proteins. chromate such as sodium or potassium chromate The invention is concerned with artificial y is usually present in a ratio between about one produced oxide coatings on aluminum, and cerll) part chromate to two parts carbonate and about tain chemical treatments for producing them; one part chromate to thirty parts carbonate. and it is not concerned with electrolytic treat- Appropriate smaller amounts of sodium or potasments for producing oxide coatings. As used slum dichromate have been employed to provide herein, the term aluminum includes pure aluthe desired chromate content in the solution. minum, commercial aluminum containing the In recent years, two improved carbonate type usual impurities, and aluminum base alloys. coating solutions have met with considerable When first prepared, chemical coating solusuccess, and the invention is applicable to them tions including those of the carbonate type as Well as to those discussed above. One of these referred to, have been found to be unsatisfactory is the carbonate-chromate-polyvinyl alcohol for production or commercial coating of al-umisolution, in which the last constituent may be num articles. Consequently, it has long been present in amounts by weight between about 0.2 customary to Work fresh solutions prellmiand 5 per cent, preferably 1 per cent. The other narily with aluminum, preferably scrap alumiis the carbonatechromate-protein solution, in num. This practice often results in delays of which the last constituent may be present as many hours in getting a new solution into proalbumen, casein, zein or gelatin in amounts by duction or commercial use. Likewise the prac- Weight between about 0.5 and 5 per cent, prefertice may require the unnecessary consumption ably 1 per cent. of otherwise useful aluminum, especially when A typical carbonate type of coating solution, scrap aluminum is not available. In any event, to which the invention is applicable, contains the practice may not always be carefully folthe following percentages by weight of coatlowed; and, for that reason and others, coatings ing constituents: heretofore produced areoften not uniform in weight, hardness or adsorptive properties, from Preferred Commercial piece to piece or from cycle to cycle, as the coat-- Range ing solution is repeatedly used.
gelmal the mention to 383331 325 3335511111:11:13:11: 313 0902313 vlde an improvement in processes for forming oxide coatings on aluminum which will permit T of the coating solutions being used, with a minipreferred amount and ff i mum of preparatory effort and expense to 0 range for the chromate have been shown, It 1s and reproduce coatings of more uniform also possible to produce satisfactory coat1ngs,un- Weight and hardness It is particularly an der certain conditions, without any chromate ject to produce more adsorptive coatings--coat- Present il'lgs that are more easily colored or dyed. One When a fresh Solutmn of the carbonate im specific object is to eliminate the necessity of 5 is first prepared, it eXtreme 1Y actlve and 'f working a'coati ng solution with aluminum prior 11am Produces a heavy relailvely Soft coatmg to use of the solution in producing coatings of that is easily markedand Smudged- Further use atisfactory commercial qua1jty of the solution produces coatings of lesser weight Cf the aqueous solutions used for chemically and greater hardness, but the solution will not forming oxide coatings on aluminum, those 00m 5 immediately prQ a d D uniform t m an u 'wg carbonate as t princoatings. Likewise, if ordinary practices are folcipal constituent have proved to be the most lowed, the coatings produced will not readily useful in the commercial arts. These solutions adsorb dyes. usually contain'about 0.5 to 6 per cent by weight The difficulties mentioned above have long .of' alkali metal carbonate, preferably sodium carbeen known, and have been partially overcome heretofore by working the solution with scrap aluminum, or other available aluminum, before putting the solution into production or commercial use. Such preliminary working of the solution takes many hours and often is permitted to consume aluminum unnecessarily, since it has been necessary in the past to work the solution with an arbitrary amount of aluminum, as roughly determined by experience. How working affects the solution is not fully understood, but the commonly accepted explanation is that some compound of aluminum isformedand dissolved in the solution, to the saturation point or beyond, in order to put the solution into condition to coat properly. It is believed thatthe aluminum is converted by the solution to a soluble complex, that the solutionbecomes saturated or supersaturated with this complex, and that then the conversion of additional aluminum causes precipitation of an aluminum compound of oxidic and hydrated nature-hydrated alumina. It has also been observed that cooling of a hot worked solution may result in precipitation of substantial amounts of this hydrated alumina, a result which is especially desirable if uniform coatings are later to be produced and reproduced in the solution, or if the coatings later produced are to be dyed. The language aluminum complex is used hereinafter to describe the aluminum conversion product, or its equivalent,
which is in solution (true or colloidal) and which is adapted to be precipitated. The language hydrated alumina is used hereinafter to describe the aluminum compound which is precipitated from the aluminum complex of the solution.
While the foregoing practice and explanation therefor have been known for many years, no successful substitute for the practice of working the solution with aluminum has been proposed heretofore, so far as is presently known. It has been supposed that commercially available aluminum oxides, hydroxides or hydrates could be added to a new coating solution so as to eliminate the working step, but such additions have been found ineffective for the purpose.
Ithas now been discovered, however, that a soluble salt of aluminum can be-dissolved in a coating solution of the carbonate type and the solution treated, either before or after or simultaneously with such addition, so as to produce therewith the desired aluminum complex in the solution, and also at least some precipitate of the desired hydrated alumina. This improvement in the coating process can be achieved, in general, by preliminarily providing in the solution (1) a soluble salt of aluminum in an amount sufiicient to increase the aluminum content thereof by at least about 0.05 per cent by weight, or more if desired, and (2) a neutralizing compound (such as an alkali metal bicarbonate or hydroxide) selected to react with the aluminum salt in solution to produce a condition of alkalinity in the solution in which there is an appreciable amount of aluminum complex of low solubility in the solution adapted to be precipitated as hydrated alumina. The neutralizingcompound is selected alumina, usually at a value near that which would be exhibited by the solution were the additions not made. They result in the formation of an appreciable amount of aluminum complex in the solution; and, especially in the case of the larger additions and when cooling is employed, they usually also result in the precipitation of an appreciable amount of hydrated alumina.
One class of soluble salts of aluminum which i can be employed in the practice of the invention is the class of soluble alkali metal aluminates. The preferred member of this class is sodium aluminate, which may be added effectively in an amount by weight of about 0.15 to 0.5 per cent,
; or more if desired, the weight being referred to sodium aluminate of 100 per cent purity. This addition increases the aluminum content of the solution by an amount on the order of that previously indicated as desirable. The neutralizing compounds best employed with the aluminates are the soluble alkali metal bicarbonates, which may be added in an amount suflicient to increase the carbonate content of the solution by about 0.1 to 0.3 per cent by weight, or more if desired. The preferred member of this class of compounds is sodium bicarbonate, which may be added effectively in an amount by weight of about 0.15 to 0.5 per cent, or more, depending on the amount of aluminate added. With the additions, the pH of the solution will be adjusted and readjusted, the aluminum complex will be formed in the solution, and thehydrated alumina will tend to be precipitated, as may be indicated by cloudiness in the solution.
It will be noted that the aluminate is alkaline in solution (tending to raise the pH of the solution), and that the bicarbonate has an acid reaction (tending to lower the pH of the solution). They react with each other insolution, producing some added alkalimetal carbonate, as well as the aluminum complex. The added carbonate does not interfere with the coating characteristics of the solution and, in fact, it merely raises the alkali metal carbonate content of the solution. If desired, the solution may be originally made up with an initial alkalimetal carbonate content less than that ultimately desired, according to the amount that will be formed in the preliminary treatment here described.
Neutralizing compounds other than the bicar bonates may also be employed with the aluminates. For example, carbon dioxide may be substituted for the bicarbonates. Likewise, the alkali metal dihydrogen phosphates, bisulphates, bisulfites, and sulfur dioxide (or sulfurous acid) may be employed. In any case these neutralizing compounds should be employed in approximately the stoichiometric amounts for the neutralizing reaction with the aluminate.
Another class of soluble salts of aluminum which can be employed in the practice of the invention is the class of soluble normalaluminum salts. The preferred member of this class is aluminum sulfate, but other similar aluminum salts such as the chloride or the. nitrate, or the like, may be found suitable. Aluminum sulfate, for example, may be added efiectively in an amount by weight of about 0.3to l per, cent, or more if desired, the weight being referred to the anhydrous salt. Hydrated aluminum sulfate will usually be employed and the corresponding larger weight of that form of aluminum sulfate would, of course, be added, the appropriate .actual weight of either form being contemplated herein. This addition likewise increases the aluminum content of the solution by an amount on the order of that previously indicated as desirable. The neutralizing compounds best employed with the normal aluminum salts are the soluble alkali metal hydroxides, which may be added in an amount sufiicient to increase the hydroxyl content of the solution by about 0.1 to 0.3 per cent by weight, or more if desired. The preferred member of this class of compounds is sodium hydroxide which may be added efiectively in an amount by weight of about 0.2 to 0.7 per cent by weight, or more, depending on the amount of normal aluminum salt added. With the additions, the pH of the solution will be adjusted and readjusted, the aluminum complex will be formed in the solution, and the hydrated alumina will tend to be precipitated, as may be indicated by cloudiness in the solution.
It will be noted that the aluminum salt in this last class is acid in solution (tending to lower the pH of the solution), and that the hydroxide is alkaline (tending to raise the pH of the solution to a point favorable to formation of the aluminum complex). They react with each other in solution, producing an alkali metal salt, as well as the aluminum complex. The alkali metal salt does not interfere with the coating characteristics of the solution, but it does not raise the alkali metal carbonate content of the solution.
Soluble aluminum salts other than the normal salts may also be added to the solution. When an acid aluminum salt is employed, additional hydroxide is needed in the solution to neutralize the aluminum salt. The provision of an acid salt and the necessary additional hydroxide in the solution is equivalent to the provision of a normal salt in the solution. When a basic aluminum salt is employed, part of the hydroxide required in the solution is supplied by the hydroxide content thereof. The provision of part of the hydroxide by way of a basic salt and a smaller amount of alkali metal hydroxide is equivalent to the provision of a normal salt and a corresponding total amount of alkali metal hydroxide in the solution.
A typical coating solution including the firstmentioned class of soluble salts of aluminum might contain the following percentages by weight of coating and stabilizing constituents:
Preferred Commercial Range Sodium carbonate l. 5 0. 5-6. Sodium o'er i. 0. l 0. -2. 0 Sodium alu mate 0. 4 0v -0. 5 or more Sodium biiarbonate 0. 4 0. 15-0. 5 or more whereas a typical coating solution including the second-mentioned class of soluble salts of aluminum might contain the following percentages by it being noted that the preferred amounts of the salts of aluminum indicated contain aluminum in amounts of about 0.12 per cent by weight, referred to the weight of the solution.
With the preferred solutions given in the above examples, the adjustment and readjustment of the pH of the solution may take place as follows. If a solution of carbonate and chro mate only is first made up, it will exhibit a pH of about 11. If sodium aluminate is then added, the pH will rise above approximately 11.2. Then, if sodium bicarbonate is added, the pH will fall below about 10.5, slightly below the original value of 11. Likewise, if sodium hydroxide is first added, the pH will rise above approximately 11.6. Then, if the aluminum sulfate is added, the pH Will fall below about 10.5, slightly below the orig-- inal value of 11. Similar changes take place if? the order of adding the salt of aluminum and the: alkali, is reversed, in either case.
In either of the examples given above, the two constituents listed last may well be added last;v the chromate addition, however, may be con veniently deferred to a point after the addition of aluminate or hydroxide. As to the order, between:
themselves, of adding the two constituents listed.
last, it is desirable to add th aluminate and laterthe bicarbonate in the first example, and to add the hydroxide and later the sulfate in the second example. The stabilizing constituents are best added in the preferred amounts to a hot solution. held at temperatures above about F., prefer-- ably a solution held at about to F. Thereafter, the solution is best cooled, preferably to room temperature, to precipitate appreciable quantities of hydrated alumina. Then the solution may be reheated to temperatures suitable for coating, preferably temperature between about 175 and 195 F.
In the use of any of the solutions simply to produce ordinary oxide coatings that may be relatively hard and protective, but not necessarily uniform from piece to piece nor readily dyeable, some of the advantages of the invention may be obtained by simpl preparing a new carbonate type solution, with even the smaller indicated amounts of the soluble salt of aluminum and the neutralizing compound, preferably while the solution is hot, and directly using it to produce coatings on aluminum. This procedure at least eliminates the step of working the solution with aluminum metal.
However, in the use of an of the solutions to produce and reproduce uniform and dyeable coatings, the best results are obtained by preparing a new carbonate type solution, with the preferred or larger indicated amounts of the soluble salt of aluminum and the neutralizing compound, while the solution is hot; and, in this case, allowing the solution to cool, preferably to room temperature, by standing for several hours, preferably overnight. This fully stabilizes the solution by the precipitation of appreciable quantities of hydrated alumina. Thereafter, the solution may be heated to operating temperature and used to coat aluminum articles in the usual way. The articles coated in the stabilized solution, in successive cycles, have more uniform coatings, and the coatings dye well.
It will be seen that an improved method of utilizing carbonate type coating solutions has bee provided.
What is claimed is:
1. In a process for forming an oxide coating on aluminum by treating in an aqueous carbonate type solution containing about 0.5 to 6 per cent by weight of alkali metal carbonate,-the improvement comprising preliminarily providing in'the solution a soluble salt of aluminum in an amount sufficient to increase the aluminum content of the solution by at least about 0.05 per centb weight and a neutralizing compound reactive with the aluminum salt whereby to produce a condition of 7 alkalinity inftlie solutron ziniw'hich thereiis an n preci'able amount 'or aluminum'complex of low solubili-ty in the solution -adapted tolbe precipitated as hydrated alumina; the neutralizing compound being provided I in an amount approximating the stoichiometric amount' for the reaction with the amount of the salt f aluminum provided.
2. In a process for forming -anxoxide coating on aluminum bytreatingin an aqueous solution con taining about 0.5-ts: 6 pericent by weight of alkali metalcarbonate and aboutT0i05 to 2.0 per cent by Weight of alkali m et'al chromate, the improvement-comprising preliminarily providing in the solution a soluble salt of aluminum in an amount suiiicientto' increase the aluminum content of the solution byat least about 0.05 per cent by weight and a neutralizingcompound reactive with the aluminum salt whereb to produce a condition of alkalinity in the solution in. which there is an appreciable amount'of aluminum complex of low solubility in the solution adapted to' be precipitated as hydrated-alumina, the neutralizing compound being providedin an amount approximating the stoichiometric amount for the reaction with the amount of the salt of aluminum provid'cdQ 3. In a-process for'forming an oxide coating on aluminum by tl'eating'lnan aqueous solution containing-about 0.5 to 6 percent b weight of alkali metal carbonate; up. to about 2.0 per cent by weight of alkali metal chromate, and about 0.2 to per cent by-weight of polyvinyl alcohol, the improvement comprising preliminarily providing in the solution a; soluble salt of aluminum in an amount sufiicient'to increasethe aluminum con tentof thesolution by at least about 0.12 per cent b weight and a; neutralizing compound reactive with the aluminum salt whereby to produce a condition of alkalinity in the solution in which there is an appreciable amount of aluminum complex of low solubility in the solution adapted to be precipitated as'hydrated alumina; the neutralizing compound'being provided in an amount approximating the stoichiometric amount for the reaction with the amount of thesalt of aluminum provided.
4. In a pi'ocessforiorming an oxide coating on aluminum'b'y treating inan aqueous solution containing about 0.5 to16' percent'by weight of alkali metal carbonate, up to about 2.0 per cent by weight-of'alkali metal chromate, and about 0.5 to' 5 percent by weight of ati least one protein selected'from the'group consisting of casein, albumen, zein and. gelatin, the improvement'comprising preliminarily providing in the solution a soluble salt of aluminum inan amount sufficient to increase the aluminum content of the solution byat least about 0.12per cent by weight and a neutralizing compound reactive with the aluminum salt whereby-to. produce a condition of. alkalinity in the solution in which there is an appreciable amount of aluminum complex of" low solubility in, thesolution adapted to'beprecipitated as hydrated alumina, the neutralizingcompound being provided in an'amountrapproximatingthe. stoichiometrio. amount for the; reaction with the amount ofthe salt ofaluminum provided.
5. In a processfcr'forming an oxide coating on alum inurn by treating in a hot aqueous carbonate typo solution containingaboutO to 6. per cent byweight of alkali metal carbonate, the improvement comprising preliminarily providing the hot solution. a soluble salt-of aluminum in an amount sufiicient to increasethealuminum con.-
aiuo igce i tentz'of the soluti'on-by atileast about" 0.12 per cent by weight'and'a.neutralizing" compound re active with the aluminum salt whereby to pro duce a condition ofii'alkalinity in the solutionin which there is an appreciable amount of aluminum complex or" low solubility in the solution adapted to be precipitated ashydrated alumina, the neutralizing compound beingprovided in an amount approximating the stoichiometric amount for the reaction withthe'amount of the salt of aluminum provided, then cooling the solution toabout room temperature so as to facilitate precipitation. ofani' appreciable amount' of hydrated alumina, and then reheating thesolution for coating.
6. In aprocess .for forming an. oxide coating on aluminum by treating inanaqueous solution containing abouttldto 6"per cent by weight of alkali metal carbonate, the improvementcomprising preliminarily providing: in the solution a soluble alkali metal aluminate' in an amount sufficient to increase the aluminum content of the solutionbyat' least about 0.05 per cent by weight and a soluble alkali metal bicarbonate in an amount sufficient to? increase the carbonate content of the solution by at least about 0.1 per cent by weight; the. alkali metalbicarbonate being provided in an amount approximating the stoichiometric amount for reaction with the amount of alkali metal aluminate provided so that an appreciable amount of "aluminum complex of low solubility'is formed 'in the solution adapted to be precipitated as hydrated alumina.
'7. In a process'for forming an oxide coating on aluminum by treating 'in an aqueous solution containing about"0.5 to 6 per. centby weight of alkali metal carbonate, the improvement comprising preliminarily providing in the solution about 0.15' to 0.5 per cent by weight of sodium aluminate and about 0.15 to 0.5 per cent by' weight 0. sodium bicarbonate so that an appreciable amount of aluminum complex of low solubility is formed in the solution adapted" to be precipitated as hydrated alumina.
8. In a process for forming an oxide coating on aluminum by treating in a hot aqueous solution containing about-1.5 to 2 percent by weight of sodium carbonate and upto about 0.75 to 1 per cent by weight of alkali metal chromate, the improvement comprising preliminarily providing in the hot solution about 0.4 per cent by weight of sodium aluminate and about 0.4 per cent by weight of sodium bicarbonate, so that an appreciable amount of aluminum complex of low solubility is formed in the solution adapted to be precipitated as hydrated alumina, then cooling the solution toi about roomv temperature so as to facilitate precipitation. of an appreciable amount of hydrated alumina, and then reheating the solution for coating.
9. In a process for forming an oxide coating on aluminum by treating in an aqueous solution containing about 0.5 to 6 per cent by weight of alkali metal carbonate, the improvement comprising preliminarily providing in the solution a soluble normal aluminum salt in an amount sufficient to increase the aluminum content of the solution by at least about/0.05 per cent'by Weight and a soluble alkali metal hydroxide in an amount suflicient to increase thehydroxyl content of the solution by. at'least about 0.1 per cent by weight, the alkali metalhydroxid'e-being provided in an amount approximatingthe stoichiometric amount for reaction with the: amount of normal aluminumsalt provided, so that anzappreciableamount of aluminum complex of low solubility is formed in the solution adapted to be precipitated as hydrated alumina.
10. In a process for forming an oxide coating on aluminum by treating in an aqueous solution containing about 0.5 to 6 per cent by weight of alkali metal carbonate, the improvement comprising preliminarily providing in the solution about 0.3 to 1 per cent by weight of aluminum sulfate and about 0.2 to 0.7 per cent by weight of sodium hydroxide, so that an appreciable amount of aluminum complex of low solubility is formed in the solution adapted to be precipitated as hydrated alumina.
11. In a process for forming an oxide coating on aluminum by treating in a hot aqueous solution containing about 1.5 to 2 per cent by weight of sodium carbonate and up to about 0.75 to 1 per cent by weight of an alkali metal chromate. the improvement comprising preliminarily providing in the hot solution about 0.8 per cent by weight of aluminum sulfate and about 0.5 per cent by weight of sodium hydroxide, so that an appreciable amount of aluminum complex of low solubility is formed in the solution adapted to be precipitated as hydrated alimiina, then cooling the solution to about room temperature so as to facilitate precipitation of an appreciable amount of hydrated alumina, and then reheating the solution for coating.
RALPH B. MASON.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Industry, vol. II, page 58, McGraw-Hill, New York, 1930.

Claims (1)

1. IN A PROCESS FOR FORMING AN OXIDE COATING ON ALUMINUM BY TREATING IN AN AQUEOUS CARBONATE TYPE SOLUTION CONTAINING ABOUT 0.5 TO 6 PER CENT BY WEIGHT OF ALKALI METAL CARBONATE, THE IMPROVEMENT COMPRISING PRILIMINARILY PROVIDING IN THE SOLUTION A SOLUBLE SALT OF ALUMINUM IN AN AMOUNT SUFFICIENT TO INCREASE THE ALUMINUM CONTENT OF THE SOLUTION BY AT LEAST ABOUT 0.05 PER CENT BY WEIGHT AND A NEUTRALIZING COMPOUND REACTIVE WITH THE ALUMINUM SALT WHEREBY TO PRODUCE A CONDITION OF ALKALINITY IN THE SOLUTION IN WHICH THERE IS AN APPRECIABLE AMOUNT OF ALUMINUM COMPLEX OF LOW SOLUBILITY IN THE SOLUTION ADAPTED TO BE PRECIPITATED AS HYDRATED ALUMINA, THE NEUTRALIZING COMPOUND BEING PROVIDED IN AN AMOUNT APPROXIMATING THE STOICHIOMETRIC AMOUNT FOR THE REACTION WITH THE AMOUNT OF THE SALT OF ALUMINUM PROVIDED.
US724923A 1947-01-28 1947-01-28 Forming oxide coatings on aluminum Expired - Lifetime US2504434A (en)

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FR953601D FR953601A (en) 1947-01-28 1947-09-29 Improvements in the stabilization of aqueous solutions of the type of carbonate solutions intended for the formation of oxide coating on aluminum
ES0180000A ES180000A1 (en) 1947-01-28 1947-10-04 A PROCEDURE FOR STABILIZING AN AQUEOUS SOLUTION OF THE CARBONATE TYPE, USED TO FORM LAYERS OF OXIDE ON ALUMINUM

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US3280734A (en) * 1963-10-29 1966-10-25 Howard A Fromson Photographic plate
US3287179A (en) * 1963-01-04 1966-11-22 Frank Theodore Process for preparing aluminum surfaces prior to plating
US4705639A (en) * 1985-05-10 1987-11-10 The United States Of America As Represented By The Secretary Of The Air Force Ferrous and sulfide treatment of electroplating wastewater

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Publication number Priority date Publication date Assignee Title
GB226776A (en) * 1923-12-29 1925-03-05 Oswald Bauer Process of producing a protective and at the same time electrically insulating coating
DE423758C (en) * 1923-12-29 1926-01-09 E H Oswald Bauer Dr Ing Process for producing a protective and at the same time electrically insulating coating on aluminum
US1965269A (en) * 1931-05-01 1934-07-03 Aluminum Co Of America Method of coloring aluminum
US2106368A (en) * 1935-11-08 1938-01-25 Addressograph Multigraph Sheet aluminum planographic plate
US2129071A (en) * 1935-10-31 1938-09-06 Addressograph Multigraph Planographic printing plate
US2337940A (en) * 1943-03-25 1943-12-28 Aluminum Co Of America Method of treating aluminum surfaces
US2464596A (en) * 1945-02-15 1949-03-15 Aluminum Co Of America Chemical method of coating aluminum
US2466971A (en) * 1945-02-15 1949-04-12 Aluminum Co Of America Method of chemically coating aluminum

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Publication number Priority date Publication date Assignee Title
GB226776A (en) * 1923-12-29 1925-03-05 Oswald Bauer Process of producing a protective and at the same time electrically insulating coating
DE423758C (en) * 1923-12-29 1926-01-09 E H Oswald Bauer Dr Ing Process for producing a protective and at the same time electrically insulating coating on aluminum
US1965269A (en) * 1931-05-01 1934-07-03 Aluminum Co Of America Method of coloring aluminum
US2129071A (en) * 1935-10-31 1938-09-06 Addressograph Multigraph Planographic printing plate
US2106368A (en) * 1935-11-08 1938-01-25 Addressograph Multigraph Sheet aluminum planographic plate
US2337940A (en) * 1943-03-25 1943-12-28 Aluminum Co Of America Method of treating aluminum surfaces
US2464596A (en) * 1945-02-15 1949-03-15 Aluminum Co Of America Chemical method of coating aluminum
US2466971A (en) * 1945-02-15 1949-04-12 Aluminum Co Of America Method of chemically coating aluminum

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3287179A (en) * 1963-01-04 1966-11-22 Frank Theodore Process for preparing aluminum surfaces prior to plating
US3280734A (en) * 1963-10-29 1966-10-25 Howard A Fromson Photographic plate
US4705639A (en) * 1985-05-10 1987-11-10 The United States Of America As Represented By The Secretary Of The Air Force Ferrous and sulfide treatment of electroplating wastewater

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ES180000A1 (en) 1947-11-16

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